Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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LOW-VOC POLYAMINO ALCOHOLS
Background
This invention relates generally to a polyamine compound useful in coating
compositions and other applications for pH adjustment.
Compounds with multiple amino and/or hydroxyl groups are known. For example,
M. Senkus, J. Am. Chem. Soc. (1946), 68, 10-12, discloses a compound having
the formula
H2N X"'I OH
N
xx^'~ H
but this reference does not disclose or suggest a polyamino-polyalcohol
compound as claimed
in the present application.
The problem addressed by this invention is to find new low VOC polyamine
compounds useful in coating compositions and other applications for pH
adjustment.
Statement of Invention
The present invention is directed to a method for producing a polyamino-
polyalcohol.
The method comprises steps of: (a) combining an aminoalcohol of formula (I)
R2 R3
HO
X NHR1
R4 (I)
with a nitro-diol of formula (II)
HO OH
R5 NO2 (II)
wherein R' is hydrogen, hydroxyethyl or C1-Clo alkyl; R2 and R3 independently
are
hydrogen, methyl, ethyl, hydroxymethyl, or R2 and R3 combine with a carbon to
which they
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are attached to form a five-membered or six-membered saturated carbocyclic
ring; R4 is
hydrogen or C1-C4 alkyl; R5 is methyl or ethyl; to produce a nitro amino diol;
and (b)
contacting said nitro amino diol with a reducing agent capable of reducing
aliphatic nitro
groups.
The present invention is further directed to a compound having formula (III)
R2 R3
HO
N OH
R4 R6 R5 N(R')2 (III)
wherein R2 and R3 independently are hydrogen, methyl, ethyl, hydroxymethyl, or
R2 and R3
combine with a carbon to which they are attached to form a five-membered or
six-membered
saturated carbocyclic ring; R4 is hydrogen or C1-C4 alkyl; R5 is hydrogen,
methyl, ethyl or
hydroxymethyl; R6 is hydrogen, hydroxyethyl, C1-C10 alkyl or -
CH2C(R5)(N(R7)2)CH2OH;
and R7 is hydrogen or methyl.
The present invention is further directed to a compound having formula (IV)
R2 R3
HO
X N ~OH
R4 R6 R5 N02
(IV)
wherein R2 and R3 independently are hydrogen, methyl, ethyl, hydroxymethyl, or
R2 and R3
combine with a carbon to which they are attached to form a five-membered or
six-membered
saturated carbocyclic ring; R4 is hydrogen or C1-C4 alkyl; R5 is hydrogen,
methyl, ethyl or
hydroxymethyl; R6 is hydrogen, hydroxyethyl, C1-C1o alkyl or-
CH2C(R5)(N02)CH2OH.
The present invention is further directed to a compound having formula (V)
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R2 R3 R3 R2
HO OH
X N N
1 RS
R4 R6 N(R7)2 R6 R4 (V)
wherein R2 and R3 independently are hydrogen, methyl, ethyl, hydroxymethyl, or
R2 and R3
combine with a carbon to which they are attached to form a five-membered or
six-membered
saturated carbocyclic ring; R4 is hydrogen or C1-C4 alkyl; R5 is hydrogen,
methyl, ethyl or
hydroxymethyl; R6 is hydrogen, hydroxyethyl, C1-C10 alkyl or -
CH2C(R5)(N(R7)2)CH2OH;
and R7 is hydrogen or methyl.
The present invention is further directed to a compound having formula (VI)
R2 R3 R3 R2
HO OH
X N N
R4 16 R5 NO2 R6 R4 (VI)
wherein R2 and R3 independently are hydrogen, methyl, ethyl, hydroxymethyl, or
R2 and R3
combine with a carbon to which they are attached to form a five-membered or
six-membered
saturated carbocyclic ring; R4 is hydrogen or C1-C4 alkyl; R5 is hydrogen,
methyl, ethyl or
hydroxymethyl; R6 is hydrogen, hydroxyethyl, C1-C10 alkyl or-
CH2C(R5)(NO2)CH2OH.
Detailed Description
All percentages are weight percentages ("wt%"), unless otherwise indicated.
Concentrations in parts per million ("ppm") are calculated on a weight/volume
basis. An
"aqueous" composition is one comprising at least 30 wt% water, preferably at
least 35 wt%
water, preferably at least 38 wt% water. Preferably, aqueous compositions
comprise no more
than 5 wt% organic solvent. An "alkyl" group is a hydrocarbyl group having
from one to
twenty carbon atoms, unless otherwise specified, in a linear or branched
arrangement. Alkyl
groups optionally have one or more double or triple bonds. Substitution on
alkyl groups of
one or more hydroxy or alkoxy groups is permitted. Preferably, alkyl groups
are saturated
and unsubstituted. A difunctional group is a substituent group having two
points of
attachment, e.g., one example of a difunctional alkyl group would be -(CH2),,
, where x could
be from two to twenty.
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In the method of this invention, preferably R' is hydrogen; R2 and R3
independently
are hydrogen, methyl or ethyl; R4 is hydrogen; and R5 is hydrogen, methyl or
ethyl.
Preferably, R5 is methyl. Preferably, R2 and R3 are methyl.
In the compounds of this invention, preferably R2 and R3 independently are
hydrogen,
methyl or ethyl; R4 is hydrogen; R5 is hydrogen, methyl or ethyl; and R6 is
hydrogen or
-CH2C(R5)(N(R7)2)CH2OH (in compounds III and V) or -CH2C(R5)(N02)CH2OH (in
compounds IV and VI). Preferably, R2 and R3 are methyl. Preferably, R4 is
hydrogen.
Preferably, R5 is methyl. Preferably, R6 is hydrogen.
In some embodiments of the invention, R2 and R3 combine with a carbon to which
both are attached to form a five-membered or six-membered saturated
carbocyclic ring, i.e.,
R2 and R3 together represent a C4-C5 difunctional group having formula -(CH2)4-
or
-(CH2)5-. For example, in compound (I) when R2 and R3 represent -(CH2)5-, the
structure
would be
HO
NHR1
R4
Reduction of nitro compounds (IV) and (VI) may be accomplished using any
reagent
capable of reducing aliphatic nitro groups. Examples of such reducing agents
include
hydrogen gas in combination with a catalyst, for example, Raney nickel, a
platinum or
palladium based catalyst (Pt or Pd in elemental form or as oxides, with or
without supports
e.g. carbon); and other reducing agents including metal/acid combinations,
e.g. iron/acetic
acid; and aluminum hydrides, e.g., VITRIDE. Preferred reducing agents include
hydrogen
gas in combination with any of the following catalysts: Raney nickel, Platinum
or palladium.
Conditions for hydrogenation of nitro groups are well known, e.g., a
temperature range of
about 20-80 C at a pressure of about 100-1000 psi (690 - 6900 kPa) and these
can be
adjusted easily by one skilled in the art. Reduction of these compounds in the
presence of
excess formaldehyde and temperature between 60-140 C, reduces the aliphatic
nitro groups
to dimethylamino groups instead of amino groups, corresponding to R7=methyl in
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compounds (III) and (V). Preferably, formaldehyde is present in 100-200% of
the
stoichiometric amount required to fully methylate the amines present in the
reduced
compound. Reduction without formaldehyde will produce compounds having
R7=hydrogen.
Preferably, compound (VI) is prepared using a molar ratio of compound (I) to
5 compound (II) of approximately two:one, resulting in one mole of compound
(I) becoming
attached to each end of compound (II). Preferably, the molar ratio of (I) to
(II) is from 2.3:1
to 1.5:1, preferably from 2.1:1 to 1.8:1. However, if the ratio of compound
(I) to compound
(II) is approximately one:two, then compound (IV) in which R6 is
CH2C(NO2)(R')(CH2OH)
will be formed. In this case, clearly R1 in compound (I) must be hydrogen.
Preferably, if
compound (IV) in which R6 is CH2C(NO2)(R')(CH2OH) is desired, the molar ratio
of (I) to
(II) is from 1:1.5 to 1:2.3, preferably from 1:1.8 to 1:2.1. Preferably, if
compound (IV) in
which R6 is hydrogen, hydroxyethyl or C1-Clo alkyl is desired, then the molar
ratio of
compound (I) to compound (II) is approximately one:one. Preferably, the molar
ratio of (I) to
(II) is from 1.2:1 to 0.8:1, preferably from 1.1:1 to 0.9:1.
When the compound of formula (III) or (V) is used to adjust pH in an aqueous
coating
composition or other aqueous composition having an initial pH less than 7, the
amount of
compound added clearly can vary depending on the initial pH, desired final pH,
and other
components present in the composition. However, one skilled in the art can
easily determine
the necessary amount of these compounds to be added. In acrylic latex coating
compositions,
typically the amount would be in the range from 10 wt% to 125 wt% of total
weight of
carboxylic acid groups in the coating composition, alternatively from 25 wt%
to 100 wt%.
In some embodiments of the invention, the initial pH of the aqueous
composition is from 2-7,
alternatively from 2.5-6. The target pH value preferably is from 7.8 to 9.5,
alternatively from
8 to 9.2. In some embodiments of the invention, the aqueous coating
composition is an
acrylic latex comprising copolymers of acrylic or methacrylic acid with C1-C8
alkyl acrylates
or methacrylates. In some embodiments of the invention, the acrylic latex
comprises 40-65
wt% polymer solids, alternatively 45-62 wt%, alternatively 45-55 wt%.
Conditions for reaction of compounds (I) and (II) are generally known, e.g.,
typically
the reactants are heated to reflux for 1-14 hours and then optionally kept at
room temperature
(20-25 C) for up to 24-48 hours. There are many suitable solvents, e.g.,
water, methanol,
ethanol, and mixtures thereof.
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Example 1:
NO2 N02 H NO
HOTOH + OH r.t'50 CHO z HO Z
H2N H~H + HT(2) N\_O
(~> A
500 mL 3-neck flask equipped with a magnetic stirrer, nitrogen blanket,
thermocouple
controlled heating mantle and addition funnel is charged with 2-ethyl-2-
nitropropane-1,3-diol
(69.2 wt% NEPD in water: 72.3 g/0.336 moles, lequivalent). The addition funnel
is
charged with 2-amino-2-methylpropan-l-ol, AMP-95 (89% AMP: 67.2 g/0.671 moles,
2equivalents). The AMP added to the NEPD solution over a period of 30 minutes,
while
stirring under a nitrogen blanket. A mild exotherm is noted at the beginning
of the addition.
The reaction was stirred overnight at room temperature, followed by heating
the reaction
mixture to 500 C for additional 8-10 hrs. The yellow solution turned brown
upon heating.
LC/MS analysis of the reaction showed a mixture of two compounds. The major
product was
compound (2) i.e., 2-(2-((4,4-dimethyloxazolidin-3-yl)methyl)-2-
nitrobutylamino)-2-
methylpropan-1-ol, [M+H] = 304.22 and the minor product was compound (1) with
[M+H] _
292.22. The reaction mixture was taken as-is and hydrogenated
Example 2:
HO
HO2V NH2 /__/OH HO ~NH N
H O N N O H H N +
T ~NH > H
H H H2, 600 psi (3)
(4)
MeOH, Raney Ni (cat)
+ NH2 + NH2
TY N O 2 H O N N HOv 'N NY
HO,_ ~ N N1 1 HO H HO
H O 6
(5) ( )
A 2-liter Parr autoclave is charged with methanol (300 mL) and Raney Nickel
catalyst (R-
3111, 16.3 g wet weight). The reactor is sealed, purged with nitrogen followed
by purging
with hydrogen and then brought up to 60 C under 426 psi hydrogen pressure.
When the
temperature reaches the desired mark, the reactor pressure increased to
approximately 600
psi. With rapid stirring (600-640 rpm), the reaction mixture from above -
diluted with an
additional 50 mL of methanol and added over a period of 30 minutes while
maintaining the
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reactor at 60 C/600 psi hydrogen. When the addition is completed, the
autoclave temperature
is increased to 100 C and temperature maintained for 30 minutes. Followed by
temperature
increase to 110 C for additional 30 minutes; finally, the temperature ramped
up to 120 C and
reaction mixture in the autoclave stirred for 90 minutes at that temperature
to ensure complete
opening of the oxazolidine ring. At this point, the reaction deemed complete.
After cooling to
room temperature, the reactor is vented, opened and the crude product isolated
via vacuum
filtration. The brown filtrate is stripped on a rotary evaporator (50-55 C /
29-30" vacuum) to
remove water/methanol. The process resulted in approximately 16.68 g of
viscous brown
product. GC-MS characterized the products as a mixture of four poly-amino
alcohols.
Compound (3), [M+H] = 262; Compound (4), [M+H] = 276; Compound (5), [M+H] =
290
and Compound (6), [M+H] = 276.
Example 3:
O2N H
HO N~N OH
NO2
(7) Major
HO OH + H2N~NH2
O2N +
O2N H
HO N~N'O
O2N `'
(8) Minor
A 250 mL 1-neck flask equipped with a magnetic stirrer, nitrogen blanket and
addition funnel
is charged with 2-ethyl-2-nitropropane-1,3-diol (69.2 wt% NEPD in water: 73.4
g/0.341
moles, 2equivalent). The addition funnel charged with 2-methylpropane-1,2-
diamine, MDP
(15 g/0.170 moles, 1 equivalent). The MDP added slowly to the NEPD solution,
while
stirring under a nitrogen blanket. Upon addition of MDP, the clear yellow
solution turned
murky. Stirring the reaction mixture overnight, resulted in two layers i.e.,
the aqueous layer
and a gel like layer. The aqueous layer was decanted and -59 g of gel like
yellow material
obtained. The LC-MS analysis showed the desired product i.e., compound (7),
[M+H] =
351.22 and compound (8) the oxazine, [M+H] = 362.22 as the major products. The
mono
addition product also detected. The reaction mixture was taken as-is and
hydrogenated.
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Example 4:
O2N H H2N H
HON N OH HO N
H NO2 H NH2OH
~~
(7) Major (9) Minor
+ H2, 600 psi +
02N Raney Nickel (cat) H
HO 2N H NKN^O HOH2N NXN^O
02N `~ H2N `' (8) Minor (10) Major
A 2-liter Parr autoclave charged with methanol (300 mL) and Raney Nickel
catalyst (R-3111,
12 g wet weight). The reactor is sealed, purged with nitrogen followed by
purging with
hydrogen and then brought up to 60 C under 600 psi hydrogen pressure. With
rapid stirring
(600-620 rpm), the reaction mixture from above diluted with an additional 100
mL of
methanol and added over a period of 30-45 minutes while maintaining the
reactor at
60 C/600 psi hydrogen. The reaction deemed complete, when the hydrogen uptake
by the
reaction stopped. After cooling to room temperature, the reactor vented,
opened and the crude
product isolated via vacuum filtration. The yellow filtrate is stripped on a
rotary evaporator
(50-60 C / 29-30" vacuum) to remove water/methanol. The process resulted in
34.6 g of
slightly viscous product. LC-MS characterized the products as a mixture of
Compound (9),
[M+H] = 291.27 and Compound (10), [M+H] = 303.27. The major product was the
poly
amino oxazine, compound (10). There is formation if six member ring during
hydrogenation.
The ring forms when amine reacts with formaldehyde by release water. The
source could be
from excess formaldehyde in aqueous NEPD or reversal of the nitro amino
alcohol.
Example 5:
NO2 NO2 ~OH
HO OH + H2N" vOH HO H
(11)
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A 100 mL 1-neck flask equipped with a magnetic stirrer, nitrogen blanket and
addition funnel
is charged with 2-ethyl-2-nitropropane-1,3-diol (69.2 wt% NEPD in water: 36.2
g/0.167
moles, 1 equivalent). The addition funnel charged with 2-amino-2-methylpropan-
l-ol, AMP-
95 (89% AMP: 8.35 g/0.084 moles, 0.5 equivalents). The AMP added to the NEPD
solution
over a period of 10 minutes, while stirring under a nitrogen blanket. A mild
exotherm noted
at the beginning of the addition. The reaction let to stir for 24 hrs at room
temperature. The
clear yellow solution turned opaque and milky upon stirring for 24 hrs. LC-MS
analysis
showed that the desired product i.e., 2-((1-hydroxy-2-methylpropan-2-
ylamino)methyl)-2-
nitrobutan-1-ol, compound (11) was the major product with [M+H] = 221.14 and
small
amount of 2-(2-((4,4-dimethyloxazolidin-3-yl)methyl)-2-nitrobutylamino)-2-
methylpropan-l-
ol, [M+H] = 304.22. There were few low boiler impurities detected also and
will be removed
after hydrogenation reaction. The reaction mixture was taken as-is and
hydrogenated.
Example 6:
NO2 Y__/ OH H2, Y__/ OH
HO TN , 600 psi HO N
H MeOH, Raney Ni (cat) H
(11) (12)
A 300 mL Parr autoclave charged with methanol (100 mL) and Raney Nickel
catalyst (R-
3111, 11.4 g wet weight). The reactor is sealed, purged with nitrogen followed
by purging
with hydrogen and then brought up to 60 C under 700-740 psi hydrogen pressure.
With rapid
stirring (600-620 rpm), the orange reaction mixture from above diluted with an
additional 100
mL of methanol and added over a period of 30-45 minutes while maintaining the
reactor at
60 C/700 psi hydrogen. After 45 min of stirring at 60 C, the autoclave
temperature increased
to 70 C/735 psi, and stirred under hydrogen pressure for another 30 minutes.
The temperature
of the autoclave was further increased to 90 C/761 psi and the reaction
mixture stirred for an
additional 45 minutes. The reaction deemed complete, when the hydrogen uptake
by the
reaction stopped. After cooling to room temperature, the reactor vented,
opened and the crude
product isolated via vacuum filtration. The yellow filtrate is stripped on a
rotary evaporator
(50-60 C / 29-30" vacuum) to remove water/methanol. The process resulted in
10.6 g of
yellow viscous product. Cl GC/MS characterized the products as Compound (12),
2-amino-2-
((1 -hydroxy-2-methylpropan-2-ylamino)methyl)butan- 1-01, with retention time
of 17.7 min
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and [M+H] = 191 as the major component. There was a peak for AEPD as a result
of using
excess NEPD during the Mannich reaction (example 5). The other minor
impurities were the
methylated amino alcohol products.
